Thermoplastic polymer compositions containing high molecular weight poly(vinyl aromatic) melt-rheology modifiers

ABSTRACT

Vinyl aromatic polymers having a minimum molecular weight of about 500,000, and preferably of about 1,500,000, are blended at levels of from about 1 to about 25% with thermoplastic resins to improve the melt rheology of the thermoplastic resins and facilitate blow molding, thermoforming, extrusion and similar processes.

This is a divisional of application Ser. No. 389,662, filed Aug. 4, 1989now U.S. Pat. No. 5,102,952.

This invention relates to melt-rheology modifiers for thermoplasticpolymers, and more particularly to high-molecular-weight vinyl aromaticpolymers as melt-rheology modifiers, and to the thermoplastic polymershaving modified melt-rheology properties.

BACKGROUND OF THE INVENTION

The modified thermoplastic polymer compositions of the present inventionare particularly well suited to blow-molding processes, by whichthin-walled articles such as bottles of all sizes are formed from apartially shaped, usually hollow polymer article known as a parison. Theparison is formed by well-known processes such as extrusion or injectionmolding; it is then typically placed in a final mold, expanded by gaspressure to conform to the shape of the final mold and cooled to fix itsshape. Variations of this process are well known in the art, and it maybe used with many thermoplastic polymers. Such polymers that have beenused by others to form blow-molded articles include poly(vinylchloride), or PVC, poly(ethylene terephthalate), or PET, andpolypropylene.

Desirably, such polymers balance melt-rheology properties such as flowand sag: the polymer must flow readily enough to be extruded, injectionmolded or otherwise formed into the parison; it must be sufficientlyelastic and thermoplastic to fill the final mold readily under airpressure and heat, and without melt fracture or other surfacedistortion; yet it must be sufficiently resistant to flow or sag whilecooling that the shape of the finished article is retained.

Further, if the polymer may be crystallized, the various processing,blending, and forming operations to which it is subjected must notaccelerate crystallization to the point that blow-molding properties aredegraded.

This combination of properties is difficult to find in unmodifiedpolymers. Poly(vinyl chloride) may be easily modified with polymers thatact as processing aids to make a polymer that is tractable inblow-molding applications, but other polymers have been more difficultto modify satisfactorily. Condensation polymers such as polycarbonatesand polyamides and relatively low-molecular weight polymers such aspolyethylene terephthalate of molecular weights in the range below about20,000 have been difficult to modify for blow molding, and polycarbonateresins have proved especially difficult. It further has been difficultto blow-mold blends of engineering resins, such as polycarbonates witharomatic polyesters or with nylon, where both components are ofrelatively low molecular weight and low melt viscosity in their moltenforms.

One approach that has been used to improve the blow-molding propertiesof polycarbonate resins has been to introduce chain branching into thepolycarbonate molecule. Another has been to copolymerize thepolycarbonate with a polyester. Neither of these approaches has beenentirely successful; particular properties are improved, but the balanceof properties important to blow molding is not sufficiently improved.

Branching or increasing the molecular weight of the polymer have beenapplied to other polymers used in blow molding. Branching is taught forpoly(ethylene terephthalate), but requires careful control of meltreactivity to avoid causing processing times to be extended. Polyamideshaving reactive amine end groups may be reacted with groups on anadditive, to tie together the polyamide molecules and effectively raisethe molecular weight. This method requires careful control ofstoichiometry, and may not be suited to less reactive polymers.

The rheology of polycarbonates has been controlled by additives, but theeffects found do not corrolate with the improvement in low-shear andhigh-shear viscosity taught in the present invention.

Styrene-containing copolymers have been added to polycarbonate resins orpolyester-polycarbonate blends as impact modifiers; these copolymerstypically possess a core-shell (multi-stage) morphology, and the solubleportions of these copolymers have relatively low molecular weights,generally below about 300,000. Such impact-modifying polymers preferablycontain a core (first stage) of rubbery poly(alkyl acrylate) orpoly(butadiene) polymer or copolymer which is optionally crosslinkedand/or graftlinked, and a thermoplastic hard shell (outer stage) ofpoly(styrene-co-acrylonitrile) copolymer.

Other impact modifying polymers are methacrylate-butadiene-styreneresins, which are multi-stage polymers having a butadiene polymer orcopolymer, optionally containing vinylaromatics, as for examplesstyrenics, (meth)acrylate esters, or (meth)acrylonitrile, at levelsbelow 30% and optional crosslinking, as a first stage. One or morethermoplastic methyl methacrylate polymer stages containing styrene,lower alkyl (meth)acrylates and/or (meth)acrylonitrile and optionallyother monovinyl, monovinylidene, polyvinyl and/or poly vinylidenecomponents are polymerized onto the first stage. Such modifiers areuseful for impact-property modification of polycarbonates andpolyesters.

Similarly, staged copolymers of crosslinked poly(alkyl acrylates)core//poly(alkyl methacrylates) shell have been combined withpolycarbonates, polyesters, polyamides, and other engineering resins.Such core/shell polymers do not contain the high-molecular-weightvinylaromatic polymer of the present invention; the molecular weight ofthe extractable poly(alkyl methacrylate) phase is less than 500,000, andthe remainder is crosslinked polymer. Such polymers do not function asmelt rheology modifiers.

High-molecular-weight polymers have been added to various polymers, asfor instance the addition of high-molecular-weight styrene tothermoplastic polystyrene as a foaming-process aid, or the use ofhigh-molecular-weight copolymers of styrene with a minor amount of anitrile or (meth)acrylic ester, in combination with low-molecular-weightcopolymers of styrene with nitrile or (meth)acrylic ester and graftpolymers of styrene-methyl methacrylate on a rubbery polymer, for thepurpose of raising the softening temperature of polycarbonate resins.

It has not been disclosed that any of such high-molecular-weightpolymers will affect the melt rheology of other engineering resins orblends in a way which makes feasible blow molding and other fabricationtechnology requiring good melt strength at low shear rates.

An object of the present invention is to provide a process for improvingthe rheological properties of thermoplastic polymer melts, andparticularly the blow-molding properties of such melts. A further objectis to provide a polymeric additive which improves these rheologicalproperties. Additional objects will be apparent from the disclosurebelow.

THE INVENTION

I have discovered that high-molecular-weight homopolymers or copolymersof vinyl aromatic monomers having minimum weight-average molecularweights of about 500,000, and, preferably, of about 1,500,000, impart aparticularly advantageous balance of melt-rheology properties forvarious uses, including blow molding, making extruded articles andthermoformable sheet, and making thermoformed articles therefrom, tocertain thermoplastic polymers and copolymers. These thermoplasticpolymers and copolymers include, but are not limited to, polycarbonatesin blends with the thermoplastics listed below; aromatic polyestersincluding poly(alkylene terephthalates) such as polybutyleneterphthalate, polyethyleneterephthalate and the like; poly(aromaticketones) such as polyether ketone, polyether ether ketone, polyetherketone ketone, polyketone and the like; poly(phenylene ethers);poly(phenylene sulfides); phenoxy resins; polysulfones such aspoly(ether sulfone), poly(aryl sulfone), polysulfone and the like;poly(ether imides); poly(ether imide esters); copoly(ether imideesters); poly(ester carbonates); polyarylates such as poly(bisphenol Aisophthalate); polyimides such as poly(glutarimides); aromaticpolyimides; polyacetals; polyamides including crystalline and amorphouspolyamides; poly(amide imides); nitrile resins; poly(methyl pentene);olefin modified styrene-acrylonitrile; styrene-butadiene resins;acrylonitrile-chlorinated polyethylene-styrene resins; thermoplasticelastomers such as poly(ether esters), poly(ether amides), poly(styrenebutadiene styrenes) and poly(styrene ethylene-butylene styrenes); andcopolymers and blends of the above.

DESCRIPTION OF THE INVENTION

The melt-rheology-modifying (MRM) polymers of the present invention areprepared by free-radical polymerization of vinyl aromatic monomers tominimum molecular weights of about 500,000, and preferably of about1,500,000. At least about 50%, and more preferably at least about 70%,by weight, of the polymers comprises polymer units from an vinylaromatic monomer having the formula ##STR1## where R¹ is H or CH₃, n isfrom 0 to 2, Ar is an aromatic group of from 6 to 10 nuclear carbonatoms, and R² is the same or different substituent selected from CH₃ orC₁. Especially preferred are those monomes where R¹ is H, Ar is phenyl,n is an integer of 0 or 1, and R² is CH₃. The especially preferredpolymers of the present invention are copolymers of at least 75% byweight of styrene, and up to about 25% by weight of acrylonitrile.

As a minor component of the MRM polymers, units from othercopolymerizable vinyl monomers may be selected by those skilled in theart. Included among such copolymerizable vinyl monomers are thosebearing functional groups, as for example the carboxylic acid groupsfound in (meth)acrylic acid, as well as non-functionalized monomers suchas other vinyl aromatic monomers, vinyl esters, acrylic esters,methacrylic esters, and the like.

The MRM polymers of the present invention may be prepared by any knownpolymerization techniques, including bulk, solution, emulsion orsuspension polymerization. Preferred is conventional emulsionpolymerization, using thermal, redox or other known initiation, batchfeed or gradual feed, single or multiple staged polymerization, seededpolymerization, and similar variations of this technique which will beapparent to those skilled in the art. The emulsifier may be selectedfrom among those known to be useful in polymerizations; preferred arethose which do not degrade the color or stability of the polymer or ofthe resin to which it is added. Typical of emulsifiers for emulsionpolymerization are alkali metal and ammonium salts of fatty carboxylicacids, such as sodium oleate or sodium stearate; salts ofdisproportionated rosin acids; ethoxylated and/or propoxylated alkylphenols, such as dodecyl phenol with 1-100 ethylene oxide units; saltsof aliphatic or aromatic sulfates such as sodium lauryl sulfate; saltsof aliphatic or aromatic sulfonates, such as sodium dodecylbenzenesulfonate; sodium or potassium or ammonium dialkylsulfosuccinates;disodium salts of mono- or dialkylated diphenylether disulfonates; C₁₂-C₁₈ alkylsulfonates, sulfates, sulfonates, phosphates, or phosphonatesbased on alkylene oxide adducts of alkylated phenols, such as sodiumalkylphenol(ethylene oxide)1-100 phosphate; and many others known to theart. Combinations of emulsifiers may be employed Preferred are thosewith sufficient thermal stability that their residues in the isolatedacrylic additive can be processed into the matrix resin withoutdeleterious effects on color or stability; such emulsifiers includealkyl, aryl aralkyl, and alkaryl sulfonates, and alkyl, aryl aralkyl,and alkaryl phosphonates. Such an emulsion polymerization allows thepreparation of polymer particles having small size, narrow sizedistribution and high molecular weight, quickly and at high conversions,with minimum residual monomers. One process by which polymers of thepreferred molecular weights may be made is taught by Kotani et al. inU.S. Pat. No. 4,201,848, and other processes are known to those skilledin the art. The polymer may be easily isolated from the reaction mixtureusing known techniques.

The minimum weight average molecular weight (M_(w)) of the MRM polymersof the present invention, as measured by gel permeation chromatography(GPC) techniques, is preferably about 500,000, and more preferably about1,500,000, and still more preferably about 2,000,000 (2×10⁶). Belowthese values the contribution of the polymer to the blow-moldingproperties of the resin incorporating it is small, although benefits maybe recognized from using lower-molecular-weight MRM polymers, as forexample those with M_(w) of about 400,000. Difficulties with preparingextremely high-molecular-weight polymers create a practical upper limitof about ten million for the preferred polymer, although highermolecular weights are contemplated within the scope of the presentinvention. The preferred MRM polymers are linear or branched, but theyare not crosslinked; that is, they are soluble in organic solvents astetrahydrofuran, toluene, ethylene dichloride and the line. Within thebroader aspect of the invention, crosslinked, and especially lightlycrosslinked, polymers are also contemplated. Such crosslinking may beintroduced by the incorporation of units from polyethylenicallyunsaturated monomers into the MRM polymer, preferably at levels up toabout 5%, and more preferably from about 0.01 to about 0.5%, by weightbased on the total MRM polymer weight, or it may be introduced by othertechniques known to those skilled in the art, as for example thermalcrosslinking or various post-crosslinking techniques.

The MRM polymer of the present invention may be isolated from theemulsion in which it is formed by any of several methods, includingcoagulation, evaporation, spray drying, or devolatilizing in an extruderfollowed by pelletization. Preferred are spray drying and coagulation.

The matrix resins into which the MRM polymer of the present invention isincorporated include polycarbonates; polyesters including poly(alkyleneterephthalates); poly(aromatic ketones) such as polyether ketone,polyether ether ketone, polyether ketone ketone, polyketone;poly(phenylene ethers); poly(phenylene sulfides); phenoxy resins;polysulfones such as poly(ether sulfone), poly(aryl sulfone),polysulfone; poly(ether imides); poly(ether imide esters); copoly(etherimide esters); poly(ester carbonates); polyarylates such aspoly(bisphenol A isophthalate); polyimides such as poly(glutarimides);aromatic polyimides; polyacetals; poly(styrene) including crystalpoly(styrene) and high impact poly(styrene); polymers of vinyltoluene orpara-methyl styrene; copolymers of styrene or alkyl substituted styrenewith acrylonitrile or maleic anhydride; polyamides including crystallineand amorphous polyamides; acrylate-styrene-acrylonitrile resins;acrylonitrile-butadiene-styrene resins; poly(amide imides); nitrileresins; poly(methyl pentene); olefin modified styrene-acrylonitrile;styrene-butadiene resins; acrylonitrile-chlorinated polyethylene-styreneresins; thermoplastic elastomers such as poly(ether esters), poly(etheramides), poly(styrene butadiene styrenes) and poly(styreneethylene-butylene styrenes); and copolymers and blends of the above.Those matrix resins specifically listed above shall be indicated hereinby the term "thermoplastic engineering resins".

For most advantageous results, it is preferred that a copolymer of thevinyl aromatic monomer with a polar monomer be utilized in combinationwith a polar thermoplastic engineering resin. Thus, astyrene/acrylonitrile copolymer would give a better balance ofappearance and properties than a styrene homopolymer in blends with apolyglutarimide.

Using methods known to those skilled in the art, the MRM polymer of thepresent invention may be incorporated into the matrix resin at fromabout 1% to about 25% of the total weight of resin plus polymer. Higherlevels may be used within the scope of the present invention, but maydeleteriously affect the balance of other physical properties, such asthe heat distortion temperature, of the resin in specific applications.A more preferred range is from about 1 to about 10%, and still morepreferred is from about 5 to about 10%. The MRM polymer may, forexample, be incorporated into the resin by blending the MRM polymer, asa dry powder or pellets, with a dry powder or pellets of the matrixresin. Alternatively, if the matrix resin and the MRM polymer have beenseparately prepared as emulsions, the emulsions may be mixed andisolated as an intimate mixture by conventional methods such ascoagulation or spray drying, or as yet another alternative, theemulsions may be isolated separately and sequentially in the sameequipment, this process being termed "staged coagulation." As a lesspreferred method, the monomers used to prepare the MRM polymer may bepolymerized in the presence of the matrix polymer, but thepolymerization conditions must be carefully controlled, or the molecularweight of the resulting polymer will be too low to be fully effective.

Other additives may be incorporated into the matrix resin prior orsubsequent to incorporation of the polymer of the present invention, orthey may be incorporated simultaneously, as by coagulating or spraydrying mixed emulsions of the MRM polymer and the additives, andincorporating the resulting material into the matrix resin. Suchprocedures are conventional, and will be readily apparent to thoseskilled in the art.

These additives may include other polymers useful as impact modifiers,lubricants, flame retardants, blowing agents, antioxidants, lightstabilizers, heat stabilizers, and the like. The blends may also containfillers such as calcium carbonate, reinforcing agents such as coupledmica, fibers such as glass fibers, and the like.

The core/shell impact-property modifiers, such as those based on alkylacrylate or butadiene cores and methacrylate or styrene-acrylonitrileshells are conveniently prepared by emulsion polymerization and isolatedby any of several techniques known to those skilled in the art,including coagulation, spray drying or other evaporative techniques suchas extruder coagulation with dewatering and pelletization as taught byBortnick in U.S. Pat. No. 3,751,527. These impact-property-modifyingpolymers may be stabilized with additives during isolation and may befurther treated, as by partial fusing or pelletization, for ease ofhandling or blending The MRMs of the present invention may be combinedwith the core/shell impact-property modifier in emulsion form andco-isolated, or they may be separately admixed with the matrix resins.

Blowing agents include chemical blowing agents, such asazodicarbonamides, added to or blended with the molten polymericmixture, followed by processing of the molten blend under conditionssufficient to decompose the chemical blowing agent prior to exit of themolten polymer from the processing apparatus.

Agents also include gaseous blowing agents, such as nitrogen, added tothe molten polymer blend prior to exit of the molten polymer from theprocessing apparatus.

These chemical or gaseous blowing agents will produce a foamedblow-molded, thermoformable or thermoformed article, depending on thefabrication process chosen. By "foamed" is meant an internal foamedstructure with cell sizes sufficient to decrease weight substantially,but small and uniform enough to allow support for load-bearing from thepolymer surrounding the open cells.

A significant use of the resins which incorporate the MRM polymer of theinvention is in the preparation of useful articles by extrusion blowmolding, but the enhanced melt strength imparted by the MRM polymerswill also be advantageous in preparing useful articles by processes suchas injection blow molding, thermoforming and stamping processes onpolymer sheet, molding of foamed polymers, extrusion of profile, such asfoamed profile, sheet, rods, or tubes, and the like, performed uponresins containing the MRM polymers of this invention. The resins whichincorporate the MRM polymer will also be advantageous in otherapplications where high melt strength is a desirable property. Otheruses will be readily apparent to those skilled in the art.

Useful articles which may be made from the resins which incorporate theMRM polymer of the present invention include items for automotive use,such as bumpers, spoiler panels, dashboard panels, rear window panels,external air spoilers, seat backs, truck bed liners, wind deflectors,motorcycle fairings and skirtings and the like. Further uses may includetoys, such as tricycles, surfboards, exercise equipment, televisionhousings, other equipment housings, such as typewriter cases, and thelike. Still further uses include containers such as bottles, tanks fororganic or inorganic liquids, and the like. The formed materials may beuseful in buildings, such as decorative or tough protective panels,thermoformed panels, seating construction, pipe, profiled shapes forwindow and door construction and the like.

Foamed articles such as sheet, rods, tubes, and especially profile willbe useful where the shape retention and load-bearing properties of theengineering resin are maintained but with a lighter weight construction;such uses will include panels, equipment housing, window and doorframes, toys, automotive uses, athletic equipment, and the like. Manyother uses for such tough, heat resistant, readily blow-molded,thermoformed or otherwise processed plastics having high melt strengthwill be readily apparent to those skilled in the art.

All percentages and ratios given herein are by weight, unless otherwisestated, and all reagents are of good commercial quality unless otherwisestated.

Extrusion sag time was determined by horizontally extruding a strand ofpolymer from a Killion 25-mm extruder operating at a rate of 60 rpm,through the specified die at the specified temperature. The time for thestrand to sag to a point 1.00 meter below the die was recorded inseconds. This test is an excellent indicator of the achievement of meltstrength (low shear viscosity) adequate for the commercial processingoperations described herein.

The following abbreviations are used to indicate monomer components ofthe polymers in the following examples:

MMA--Methyl Methacrylate

EA--Ethyl Acrylate

St--Styrene

AA--Acrylic Acid

AN--Acrylonitrile

BA--n-Butyl Acrylate

BMA--n-Butyl Methacrylate

In the examples and elsewhere in the specification and claims, allratios and percentages are by weight unless otherwise indicated, and allreagents are of good commercial quality unless otherwise indicated. Inall emulsion preparations, the water used is deionized water.

The following examples are intended to illustrate the invention, and notto limit it.

EXAMPLE 1

This example illustrates the preparation of a high-molecular-weightvinyl aromatic MRM polymer having an overall composition St/MMA=55/45,and molecular weight, M_(w) =2.0×10⁶.

To a 3-neck, 5-liter flask equipped with a stirrer, reflux condenser andnitrogen sweep was added 1527 g water, 3.34 g of 10% acetic acid, and63.7 g of a 10% solution of the disodium salt of monododecyldiphenylether disulfonate as emulsifier; the emulsifier was rinsed intothe vessel with an additional 30 ml of water. The contents of the vesselwere adjusted to 46° C. A mixture of 0.01 g ferrous sulfate hydrate and0.1 g of disodium ethylenediamine tetracetic acid dissolved in 30 g ofwater was added to the reactor and stirred for two minutes. Then 47.4 gof a 1% solution of sodium formaldehyde sulfoxylate was added to thevessel. After two minutes, a mixture of 236.3 g methyl methacrylate and288.7 g styrene was added; the monomers were rinsed into the vessel withan additional 25 ml of water. After stirring for three minutes, 10 g ofa 5% solution of sodium persulfate was added to the vessel, followed by0.35 g t-butyl hydroperoxide (70% active). Polymerization was evidencedby a rise in temperature of the vessel contents, beginning about fifteenminutes after the initiator was added, with a peak temperature of about62°-65° C. The vessel contents were then cooled to 40° C. An additional116.3 g of 10% emulsifier solution were rinsed into the vessel with 30ml water, followed by 44.9 g of 1% sodium formaldehyde sulfoxylatesolution; the vessel contents were then stirred for two minutes. Amixture of styrene (536.3 g) and methyl methacrylate (438.7 g) wereadded and rinsed into the vessel with 25 ml water. The temperature wasadjusted to 36° C. and 0.48 g t-butyl hydroperoxide was added. After theexotherm peak, the vessel was cooled to room temperature, and a latexhaving 44.0% solids was removed from the vessel.

EXAMPLES 2-14

These examples illustrate the improvement in extrusion sag time when ahigh-molecular-weight styrene resin was blended with a mixture ofpolycarbonate and poly(butylene terephthalate).

The latex from Example 1, as well as those of related compositionsprepared by a similar process and described in the following examples,was isolated by spray-drying, and the resulting MRM polymers meltblended, in a 25-mm Killion extruder at 249° C., into a stabilized,43/57 blend of poly(butylene terephthalate) (PBT) having an intrinsicviscosity, measured in 60/40 phenol/tetrachloroethane, of 1.1 dl/g at25° C., with branched aromatic polycarbonate as described in U.S. Pat.No. 4,001,184, having an intrinsic viscosity, measured in methylenechloride, of 0.5 dl/g at 25° C., and marketed as Lexan 151 (PC),containing 18% (based on the PBT+PC weight) core-shell impact-propertymodifier having a core (77.5 parts) polymerized from 71 parts butadiene,3 parts styrene, 4 parts methyl methacrylate and 1 part divinylbenzene;a second stage polymerized from 11 parts styrene; and a shellpolymerized from 11 parts methyl methacrylate and 0.1 parts 1,3-butyleneglycol dimethacrylate. The molecular weight of the soluble methacrylicpolymer extracted from this modifier was below 500,000; the remainder ofthe modifier was highly crosslinked and insoluble in organic solvents.Extrusion sag times were determined for these blends, and are shown inTable I.

In all examples, 800 parts of the PC/PBT blend and 150 parts of the MBSmodifier were present. In the control (Example 14), an extra 50 parts ofthe PC/PBT blend were present; in all other cases, 50 parts of a highmolecular weight styrene copolymer were present.

                  TABLE I                                                         ______________________________________                                                                  Extrusion                                                                     Sag                                                                           Time,                                               Example Styrene Copolymer sec.     M.sub.w × 10.sup.-6                  ______________________________________                                         2 (Ex. 1)                                                                            St/MMA (55/45)    24.1     2.0                                         3      Styrene homopolymer                                                                             22.6     1.6                                         4      St/MMA (95/5)     23.3     1.9                                         5      St/MMA/BA (70/15/15)                                                                            25.5     1.6                                         6      St/MMA/MAA (70/15/15)                                                                           32.8     1.6                                         7      St/IPN (95/5)     23.7     0.8                                         8      St/MMA/AN (65/10/25)                                                                            19.6     --                                          9      St/AN (95/5)      21.4     1.3                                        10      St/AA (95/5)      25.1     1.7                                        11      St/MMA (80/20)    22.0     1.4                                        12      St/MMA/BA (60/36/4)                                                                             21.8     --                                         13      St/CHMA (80/20)   27.4     1.5                                        14      NONE (control)    15.8     --                                         ______________________________________                                         IPN is isopropyl naphthalene; CHMA is cyclohexyl methacrylate. The MRMs o     Examples 6 and 10 were prepared with sodium dodecylbenzenesulfonate as        emulsifier.                                                              

EXAMPLES 15-18

In these examples are shown the improvements in extrusion sag time whenvinylaromatic MRM polymers were added to a commercial blend believed tocontain poly(phenylene ether)//high impact polystyrene, known as NorylPX-1222 (General Electric). The MRM polymers were made by the process ofExample 1. Processing and testing for sag was measured, utilizing a1.59-mm die at a barrel temperature of 232° C. The blends contained 450parts of the matrix Noryl blend and 50 parts of the MRM. The results areshown in Table II.

                  TABLE II                                                        ______________________________________                                                                Extrusion Sag                                         Example                                                                              Styrene Copolymer                                                                              Time, sec. M.sub.w × 10.sup.-6                  ______________________________________                                        15     St homopolymer   39.6       1.6                                        16     St/MMA/MAA (80/15/5)                                                                           46.8       1.6                                        17     St/AN (75/25)    46.8       2.2                                        18     --               20.6       --                                         ______________________________________                                    

EXAMPLES 19-20

These examples illustrate improvement in sag flow time imparted to acommercial acrylonitrile-butadiene-styrene (ABS) polymer by ahigh-molecular-weight MRM polymer. The MRM polymer was that used inExample 17. The ABS polymer was supplied from Borg-Warner as CyclolacHIL-1000; it is believed to be a blend of styrene/acrylonitrilecopolymer with a graft polymer of styrene/acrylonitrile onto apoly(butadiene) rubber. Extrusion sag was measured as in Examples 15-18.The extrusion sag time for the control with no MRM additive (Example 19)was 11.3 seconds; for the blend with 10 wt. % of the MRM (Example 20),the sag time was 17.1 seconds.

EXAMPLES 21-22

These examples illustrate the ability of a MRM to enhance the meltstrength of a resin sufficient to form foam of acceptable cell size andload-bearing strength. A blend of the modifier of Example 6 (10 partsper hundred parts of matrix) with the matrix blend of polycarbonate/poly(butylene terephthalate)/ MBS impact-property modifier of Examples2-14 was prepared; the blend also contained 1 part of azodicarbonamide,a chemical blowing agent. The blend was processed in a Haake Rheocordmixer at a melt temperature of 247° C. at 60 rpm and extruded through a6.35 mm. die. On exiting the die, the strand (Example 21) foamed to adiameter of 9.9 mm. The foamed extrudate had acceptable strength andsurface. A control without the MRM processed in a similar manner(Example 22) had poorer strength and surface, and had expanded to adiameter of 8.8 mm.

I claim:
 1. A blow-molded article formed from a polymer blend whichcomprises a thermoplastic engineering resin selected from the groupconsisting of polycrbonate/aromatic polyester blends, polyesters,poly(aromatic ketones), poly(phenylene ethers), poly(phenylenesulfides), poly(aromatic sulfones), poly(ether-imides), polyactals,poly(aromatic imides) polyamides, poly(amide-imides), copolymers andblends thereof from about 1 to about 25%, based on the total weight ofthe blend, of a vinyl aromatic polymer of units of one or morecopolymerizable vinyl monomers, wherein at least 50% by weight of theunits have the formula ##STR2## where R¹ is H or CH₃, n is an integer offrom 0 to 2, Ar is an aromatic group of from 6 to 10 nuclear carbonatoms, an R² is the same or different group selected from CH₃ or Clhaving a minimum weight-average molecular weight of about 1,500,000. 2.The article of claim 1 formed by extrusion blow molding.
 3. The articleof claim 1 formed by injection blow molding.
 4. The article of claim 1wherein the article is a container.
 5. The article of claim 1 whereinthe article is an automotive bumper.
 6. The article of claim 1 whereinthe article is an automotive body panel.
 7. The article of claim 1wherein the article is an architectural wall panel.
 8. An extrudedarticle formed from a polymer blend which comprises a thermoplasticengineering resin selected from the group consisting ofpolycarbonate/aromatic polyester blends, polyesters, poly(aromaticketones), poly(phenylene ethers), poly(phenylene sulfides),poly(aromatic sulfones), poly(ether-imides), polyacetals, poly(aromaticimides), polyamides, poly(amide-imides), copolymers and blends of theabove, the blended therewith from about 1 to bout 25%, based on thetotal weight of the blend, of an vinyl aromatic polymer of units of oneor more copolymerizable vinyl monomers, wherein at least 50% by weightof the units have the formula ##STR3## where R¹ is H or CH₃, n is aninteger of rom 0 to 2, Ar is an aromatic group from 6 to 10 nuclearcarbon atoms, and R2 is the same or different group selected from CH₃ anCl, having a minimum weight-average molecular weight of about 1,500,000.9. The extruded article of claim 8 wherein the article is aprofile-extruded article.
 10. The extruded article of claim 8 whereinthe article is a sheet.
 11. The extruded article of claim 8 wherein thearticle is a rod.